圆柱-壁面交界下游湍流边界层强化传热机理研究

D. Wroblewski, Q. Xie
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引用次数: 0

摘要

在圆柱体前缘下游12倍直径范围内,实验研究了圆柱体-壁面交界处的壁面传热增强,雷诺数范围为ReD = 21,000至54,000。研究人员利用圆柱体下游完全加热的表面来提供传统的传热系数,而在未加热的表面上安装薄膜表面传感器来提供绝热传热系数。流场输运测量是用三丝雷诺热流密度探头进行的。这种增强可归因于两种效应:(1)涡旋扩散系数增加和随后湍流输运增加引起的局部流体动力效应;(2)上游加热效应,由障碍物后方区域壁面温度降低引起,并对随后下游边界层的再开发产生影响。从表面传感器获得的绝热传热系数提供了误导性的结果,因为在热量和动量输运之间的类比失败了。
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Mechanisms of Heat Transfer Enhancement in a Turbulent Boundary Layer Downstream of a Cylinder-Wall Junction
The wall heat transfer enhancement behind a circular cylinder-wall junction was investigated experimentally for Reynolds numbers ranging from ReD = 21,000 to 54,000 for locations up to 12 diameters downstream of the cylinder leading edge. Surface heat transfer was studied using a fully-heated surface downstream of the cylinder to provide traditional heat transfer coefficients, and thin-film surface sensors flush-mounted on an unheated surface to provide adiabatic heat transfer coefficients. Flow field transport measurements were obtained with a triple-wire Reynolds heat flux probe. The enhancement could be attributed to two effects: (1) a local fluid dynamic effect attributed to increased eddy diffusivity and subsequent increased turbulent transport and (2) an upstream heating effect, caused by reduced wall temperatures in the region directly behind the obstacle, and their effect on the subsequent redevelopment of the boundary layer downstream. The adiabatic heat transfer coefficients obtained from the surface sensors provided misleading results, because of the breakdown in the analogy between heat and momentum transport.
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